Next Article in Journal
Continuous Cooling Transformation of Under-Cooled Austenite of SXQ500/550DZ35 Hydropower Steel
Next Article in Special Issue
Thermophysical Model for Online Optimization and Control of the Electric Arc Furnace
Previous Article in Journal
Tribological Behavior of Boronized Fe40Mn20Cr20Ni20 High-Entropy Alloys
Previous Article in Special Issue
Toward a Simplified Arc Impingement Model in a Direct-Current Electric Arc Furnace
Article

Adaptive First Principles Model for the CAS-OB Process for Real-Time Applications

1
Cybernetica AS, Leirfossvegen 27, 7038 Trondheim, Norway
2
SSAB Europe OY, Rautaruukintie 155, 92100 Raahe, Finland
3
Adigo AS, Berghagan 3, 1405 Langhus, Norway
*
Author to whom correspondence should be addressed.
Academic Editors: Thomas Echterhof, Ko-Ichiro Ohno and Ville-Valtteri Visuri
Metals 2021, 11(10), 1554; https://doi.org/10.3390/met11101554
Received: 24 August 2021 / Revised: 21 September 2021 / Accepted: 24 September 2021 / Published: 29 September 2021
A model-based system for real-time monitoring and operational support has been developed for the Composition Adjustment by Sealed argon-bubbling with Oxygen Blowing (CAS-OB) process. The model of the system is based on a previously developed dynamic model using first principles, i.e., mass and energy balances, reaction kinetics, and thermodynamics. Adaptive estimation of state variables has been implemented using a Kalman filter to ensure that the model is able to correct for deviations between measured and calculated temperatures in real-time operation. The estimation technique reduces the standard deviation of the predicted end temperature from 19.5 °C to 5.5 °C in a data series with more than 1000 heats. The system also includes an endpoint optimisation, which calculates the amount of scrap or oxygen to be added to achieve the target temperature at the end of the heat. The model has been implemented in the Cybernetica® CENIT™ framework. The overall model can be regarded as a hybrid digital twin, where a first principles model is adapted in real time using process measurements. The system also includes user interfaces for operators where process predictions can be followed, and suggested optimised inputs are presented. The system has been deployed at two refining stations at SSAB Europe OY in Raahe, Finland. The optimized suggestions for oxygen and scrap are presented to the operators in the graphical user interface. A projected temperature profile is calculated into the near future using the planned operational procedure as well as the projected temperature profile using optimised inputs. Both profiles are displayed in the user interface. Based on these trajectories, the operator can decide on whether to follow the nominal trajectory, or the recommendation from the optimisation This will help the operators make better decisions, which in turn reduces the number of rejected heats in the CAS-OB process. View Full-Text
Keywords: real-time model; estimation; model predictive control; steel refining real-time model; estimation; model predictive control; steel refining
Show Figures

Figure 1

MDPI and ACS Style

Linnestad, K.; Ollila, S.; Wasbø, S.O.; Bogdanoff, A.; Rotevatn, T. Adaptive First Principles Model for the CAS-OB Process for Real-Time Applications. Metals 2021, 11, 1554. https://doi.org/10.3390/met11101554

AMA Style

Linnestad K, Ollila S, Wasbø SO, Bogdanoff A, Rotevatn T. Adaptive First Principles Model for the CAS-OB Process for Real-Time Applications. Metals. 2021; 11(10):1554. https://doi.org/10.3390/met11101554

Chicago/Turabian Style

Linnestad, Kasper, Seppo Ollila, Stein O. Wasbø, Agne Bogdanoff, and Torstein Rotevatn. 2021. "Adaptive First Principles Model for the CAS-OB Process for Real-Time Applications" Metals 11, no. 10: 1554. https://doi.org/10.3390/met11101554

Find Other Styles
Note that from the first issue of 2016, MDPI journals use article numbers instead of page numbers. See further details here.

Article Access Map by Country/Region

1
Back to TopTop